CN103750528B - A kind of method setting baking silk inlet water score value - Google Patents

A kind of method setting baking silk inlet water score value Download PDF

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Publication number
CN103750528B
CN103750528B CN201110459899.XA CN201110459899A CN103750528B CN 103750528 B CN103750528 B CN 103750528B CN 201110459899 A CN201110459899 A CN 201110459899A CN 103750528 B CN103750528 B CN 103750528B
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value
weight percent
moisture
moisture weight
silk
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CN103750528A (en
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李贵川
谭科军
唐毅
罗光杰
韩慧杰
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China Tobacco Guizhou Industrial Co Ltd
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China Tobacco Guizhou Industrial Co Ltd
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Abstract

Set a method of drying silk inlet water point setting value, it comprises step: 1) set environment temperature T, relative air humidity R, production equipment height above sea level H, and described parameter keeps invariable in Cigarette processing process; 2) moisture weight percent value in each node pipe tobacco is measured; 3) cigarette moisture changing value in each operation is calculated; 4) determine to dry silk inlet water point setting value Z, Z=M-X1-X2-X3-X4-X5, in described formula, M represents the central value of moisture weight percentage in cigarette.The described silk inlet water of surely drying divides the method for setting value according to the requirement of brand cigarette moisture, accurately can determine the setting value of drying silk entrance moisture, to become more meticulous adjustment, play directive function to cigarette brand later stage moisture.

Description

A kind of method setting baking silk inlet water score value
Technical field
The present invention relates to a kind of method setting moisture value, particularly a kind of method setting baking silk inlet water point setting value.
Background technology
Under normal circumstances, different for the requirement of moisture in various brand cigarette, and once cigar mill's process equipment, technological process, metrical instrument and height above sea level change, in each operation, cigarette moisture changing value also may change, therefore in last brand cigarette, moisture value is difficult to determine, in cigarette, the control difficulty of moisture value is very big, and the compliance rate of general cigarette moisture value only has 80%.
Summary of the invention
For above-mentioned the deficiencies in the prior art, the invention provides a kind of method setting baking silk inlet water point setting value.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
Set a method of drying silk inlet water point setting value, it comprises step:
1) set environment temperature T, relative air humidity R, production equipment height above sea level H, the parameter of described environment temperature T, relative air humidity R and production equipment height above sea level H keeps invariable in Cigarette processing process;
2) moisture weight percent value in each node pipe tobacco is measured, comprise cut tobacco moisture weight percent value Y1 before drying process, cut tobacco moisture weight percent value Y2 before allotment of labor's sequence is mixed after drying process, mix perfuming operation forward slip value silk moisture weight percent value Y3 after allotment of labor's sequence for three, wire process forward slip value silk moisture weight percent value Y4 is store after perfuming operation, wire feed operation forward slip value silk moisture weight percent value Y5 after storage wire process, the moisture weight percent value Y6 of silk union after wire feed operation, expanded cut tobacco moisture weight percent value P, expanded cut stem moisture weight percent value G,
3) cigarette moisture changing value in each operation is calculated, comprise drying process moisture weight percent change value X1=Y2-Y1, mix allotment of labor's sequence silk union moisture weight percent change value X2=Y3-[(Y2+AP+BG)/(A+B)] for three, perfuming operation silk union moisture weight percent change value X3=Y4-Y3, storage wire process silk union moisture weight percent change value X4=Y5-Y4, wire feed operation silk union moisture weight percent change value X5=Y6-Y5, in described formula, A represents the percentage by weight of expanded cut tobacco and cut tobacco, B represents the percentage by weight of expanded cut stem and cut tobacco,
4) determine to dry silk inlet water point setting value Z, Z=M-X1-X2-X3-X4-X5, in described formula, M represents the central value of moisture weight percentage in cigarette.
Technique scheme has following beneficial effect: according to the requirement of brand cigarette moisture, can determine the setting value of drying silk entrance moisture accurately, to become more meticulous adjustment, play directive function to cigarette brand later stage moisture.
Above-mentioned explanation is only the general introduction of technical solution of the present invention, in order to better understand technological means of the present invention, and can be implemented according to the content of description, coordinates accompanying drawing to be described in detail as follows below with preferred embodiment of the present invention.The specific embodiment of the present invention is provided in detail by following examples and accompanying drawing thereof.
Accompanying drawing explanation
Fig. 1 is the schematic flow sheet of pipe tobacco processing technology in the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present invention is described in detail.
As shown in Figure 1, a kind of method setting baking silk inlet water point setting value, it comprises step:
1) set environment temperature T, relative air humidity R, production equipment height above sea level H, the parameter of described environment temperature T, relative air humidity R and production equipment height above sea level H keeps invariable in Cigarette processing process.Because the change of above-mentioned parameter in each operation of cigarette can cause severe jamming to the determination of whole technique moisture percentage by weight, therefore once confirm suitable temperature, humidity, production equipment height above sea level, can keep described parameter constant constant in whole production procedure.
2) moisture weight percent value in each node pipe tobacco is measured, comprise cut tobacco moisture weight percent value Y1 before drying process, cut tobacco moisture weight percent value Y2 before allotment of labor's sequence is mixed after drying process, mix perfuming operation forward slip value silk moisture weight percent value Y3 after allotment of labor's sequence for three, wire process forward slip value silk moisture weight percent value Y4 is store after perfuming operation, wire feed operation forward slip value silk moisture weight percent value Y5 after storage wire process, the moisture weight percent value Y6 of silk union after wire feed operation, expanded cut tobacco moisture weight percent value P, expanded cut stem moisture weight percent value G.In above-mentioned each node, the measurement of the percentage of moisture in cut tobacco weight, is realized by measurement mechanism sample detecting, three mix allotment of labor's sequence be cut tobacco, expanded cut tobacco are mixed with expanded cut stem together with.
3) cigarette moisture changing value in each operation is calculated, comprise drying process moisture weight percent change value X1=Y2-Y1, mix allotment of labor's sequence silk union moisture weight percent change value X2=Y3-[(Y2+AP+BG)/(A+B)] for three, perfuming operation silk union moisture weight percent change value X3=Y4-Y3, storage wire process silk union moisture weight percent change value X4=Y5-Y4, wire feed operation silk union moisture weight percent change value X5=Y6-Y5, in described formula, A represents the percentage by weight of expanded cut tobacco and cut tobacco, B represents the percentage by weight of expanded cut stem and cut tobacco.By calculating cigarette moisture changing value in each operation, accurate each operation moisture weight change percentage can be obtained, in above-mentioned each operation, cigarette moisture changing value changes not quite under normal circumstances, and when other parameter constants, in each operation, cigarette moisture changing value can be considered steady state value.
4) determine to dry silk inlet water point setting value Z, Z=M-X1-X2-X3-X4-X5, in described formula, M represents the central value of moisture weight percentage in cigarette, according to the central value of moisture weight percentage in various brands cigarette, and step 3) in the X1 that calculates, X2, X3, X4, X5, the moisture weight percentage settings value of cut tobacco before overbaking silk PROCESS FOR TREATMENT can be calculated fast, if the moisture weight percentage actual value of cut tobacco does not meet the requirement of setting value before actual measurement obtains drying silk PROCESS FOR TREATMENT, cut tobacco can be processed in time, just can control the quality of cigarette so in early days.
Above a kind of method of drying silk inlet water point setting value that sets that the embodiment of the present invention provides is described in detail; for one of ordinary skill in the art; according to the thought of the embodiment of the present invention; all can change to some extent in specific embodiments and applications; therefore this description is only used in being described the embodiment of the present invention; should not be construed as limitation of the present invention, all any changes made according to design philosophy of the present invention are all within protection scope of the present invention.

Claims (1)

1. set a method of drying silk inlet water point setting value, it comprises step:
1) set environment temperature T, relative air humidity R, production equipment height above sea level H, the parameter of described environment temperature T, relative air humidity R and production equipment height above sea level H keeps invariable in Cigarette processing process;
2) moisture weight percent value in each node pipe tobacco is measured, comprise cut tobacco moisture weight percent value Y1 before drying process, cut tobacco moisture weight percent value Y2 before allotment of labor's sequence is mixed after drying process, mix perfuming operation forward slip value silk moisture weight percent value Y3 after allotment of labor's sequence for three, wire process forward slip value silk moisture weight percent value Y4 is store after perfuming operation, wire feed operation forward slip value silk moisture weight percent value Y5 after storage wire process, the moisture weight percent value Y6 of silk union after wire feed operation, expanded cut tobacco moisture weight percent value P, expanded cut stem moisture weight percent value G,
3) cigarette moisture changing value in each operation is calculated, comprise drying process moisture weight percent change value X1=Y2-Y1, mix allotment of labor's sequence silk union moisture weight percent change value X2=Y3-[(Y2+AP+BG)/(A+B)] for three, perfuming operation silk union moisture weight percent change value X3=Y4-Y3, storage wire process silk union moisture weight percent change value X4=Y5-Y4, wire feed operation silk union moisture weight percent change value X5=Y6-Y5, in described formula, A represents the percentage by weight of expanded cut tobacco and cut tobacco, B represents the percentage by weight of expanded cut stem and cut tobacco,
4) determine to dry silk inlet water point setting value Z, Z=M-X1-X2-X3-X4-X5, in described formula, M represents the central value of moisture weight percentage in cigarette.
CN201110459899.XA 2011-12-31 2011-12-31 A kind of method setting baking silk inlet water score value Active CN103750528B (en)

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104886751A (en) * 2015-05-06 2015-09-09 红云红河烟草(集团)有限责任公司 Cut tobacco shred cylinder wall temperature prediction model based on cut tobacco shred water content
CN105029672B (en) * 2015-06-24 2017-03-22 广西中烟工业有限责任公司 Precise characterization method for water at outlet of baked cut tobacco
CN111184246B (en) * 2018-11-14 2021-05-28 厦门邑通软件科技有限公司 Method and system for controlling moisture content of cut tobacco drying inlet
CN111248485A (en) * 2018-11-30 2020-06-09 湖南中烟工业有限责任公司 Method for online adjusting perfuming moisture of mixed silk

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GB1445200A (en) * 1972-08-14 1976-08-04 Industrial Nucleonics Corp Dryer control system and method
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US5383479A (en) * 1992-10-30 1995-01-24 Philip Morris Incorporated Process for adjusting the moisture content of tobacco
US5436456A (en) * 1993-10-07 1995-07-25 Brown & Williamson Tobacco Corporation Moisture meter curve calibration system
CN1656946A (en) * 2004-12-31 2005-08-24 龙岩卷烟厂 Tobacco shreds drying and moisture moving control method
CN101129215A (en) * 2006-08-25 2008-02-27 湖南中烟工业公司 Method and equipment for blending tobacco material
CN101254020A (en) * 2007-12-28 2008-09-03 上海烟草(集团)公司 Thread baking thread process control method
CN101356992A (en) * 2007-07-31 2009-02-04 武汉烟草(集团)有限公司 Downstream type tobacco-dryer exit tobacco-shred water control method
CN102090704A (en) * 2010-09-21 2011-06-15 龙岩烟草工业有限责任公司 Method for improving batch procedure capability of tobacco shred making process
CN102090708A (en) * 2010-09-10 2011-06-15 龙岩烟草工业有限责任公司 Control method for improving stability of moisture content of cut tobaccos

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1445200A (en) * 1972-08-14 1976-08-04 Industrial Nucleonics Corp Dryer control system and method
US3948277A (en) * 1972-08-18 1976-04-06 Hauni-Werke Korber & Co. Kg Method and apparatus for changing the moisture content of tobacco
GB1452664A (en) * 1973-06-07 1976-10-13 Svenska Tobaks Ab Methods of facilitatint exact evaluation and control of the processing of a product mass and apparatuses for carrying said methods into effect
US5383479A (en) * 1992-10-30 1995-01-24 Philip Morris Incorporated Process for adjusting the moisture content of tobacco
US5436456A (en) * 1993-10-07 1995-07-25 Brown & Williamson Tobacco Corporation Moisture meter curve calibration system
CN1656946A (en) * 2004-12-31 2005-08-24 龙岩卷烟厂 Tobacco shreds drying and moisture moving control method
CN101129215A (en) * 2006-08-25 2008-02-27 湖南中烟工业公司 Method and equipment for blending tobacco material
CN101356992A (en) * 2007-07-31 2009-02-04 武汉烟草(集团)有限公司 Downstream type tobacco-dryer exit tobacco-shred water control method
CN101254020A (en) * 2007-12-28 2008-09-03 上海烟草(集团)公司 Thread baking thread process control method
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